CN111350943B - Crude oil gathering and transporting method - Google Patents
Crude oil gathering and transporting method Download PDFInfo
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- CN111350943B CN111350943B CN201811562692.3A CN201811562692A CN111350943B CN 111350943 B CN111350943 B CN 111350943B CN 201811562692 A CN201811562692 A CN 201811562692A CN 111350943 B CN111350943 B CN 111350943B
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- 239000010779 crude oil Substances 0.000 title claims abstract description 157
- 238000000034 method Methods 0.000 title claims abstract description 48
- 239000003129 oil well Substances 0.000 claims abstract description 181
- 239000003921 oil Substances 0.000 claims abstract description 129
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 108
- 238000002156 mixing Methods 0.000 claims abstract description 58
- 238000004519 manufacturing process Methods 0.000 claims abstract description 53
- 238000012360 testing method Methods 0.000 claims abstract description 27
- 230000008569 process Effects 0.000 claims abstract description 15
- 230000007704 transition Effects 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 229910000831 Steel Inorganic materials 0.000 claims description 45
- 239000010959 steel Substances 0.000 claims description 45
- 239000012530 fluid Substances 0.000 claims description 10
- 238000012546 transfer Methods 0.000 claims description 10
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 239000002349 well water Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 4
- 230000009467 reduction Effects 0.000 description 5
- 230000005540 biological transmission Effects 0.000 description 4
- 230000005484 gravity Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 2
- 238000012163 sequencing technique Methods 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000000518 rheometry Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D1/00—Pipe-line systems
- F17D1/08—Pipe-line systems for liquids or viscous products
- F17D1/14—Conveying liquids or viscous products by pumping
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D3/00—Arrangements for supervising or controlling working operations
- F17D3/12—Arrangements for supervising or controlling working operations for injecting a composition into the line
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- Water Supply & Treatment (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention relates to the technical field of gathering and transporting of oil wells in oil fields, in particular to a crude oil gathering and transporting method. The method comprises the following steps: determining the gathering and transportation difficulty degree of each oil well according to the production data of each oil well in the oil field block; sequentially connecting all oil wells in the oil field block in series from high to low according to the gathering and transportation difficulty degree through an oil outlet pipeline; performing rheological property test on the crude oil, and determining a gathering, transportation and phase transition point of the crude oil, wherein the gathering, transportation and phase transition point is the water content when the viscosity of the crude oil reaches the highest point; obtaining the water mixing rate of all oil wells in the oil field block according to the oil production rate and the liquid production rate b of all oil wells in the oil field block and the gathering, transportation and phase transition point of the crude oil; and connecting the water mixing pipeline with the oil well with the highest gathering and transportation difficulty degree, and mixing water into the oil well with the highest gathering and transportation difficulty degree according to the water mixing speed, so that all the oil wells perform crude oil gathering and transportation through the oil outlet pipeline. The method can determine the water mixing amount, save materials and simplify the water mixing process.
Description
Technical Field
The invention relates to the technical field of gathering and transporting of oil wells in oil fields, in particular to a crude oil gathering and transporting method.
Background
The crude oil has high content of colloid asphaltene, few light fractions, high density and viscosity, poor fluidity and difficult ground transportation, and needs to take measures to reduce viscosity for transportation.
The commonly used viscosity reduction conveying method comprises a double-pipe water mixing method, a heating method, a diluting method, a modification viscosity reduction method, an emulsification viscosity reduction method and a chemical viscosity reduction method, wherein the double-pipe water mixing method is applied more frequently. The double-pipe water mixing method mixes a large amount of hot water, active water or sewage into crude oil, thereby achieving the purposes of viscosity reduction and convenient transportation. The produced water separated from crude oil treatment in the combined station is pressurized by a pump and heated by a heating furnace, then is conveyed to the wellhead of the oil well through a water mixing pipeline, is mixed with produced liquid of the oil well at the wellhead and then is conveyed outside through an oil outlet pipeline, and each oil well needs to be matched with one water mixing pipeline and one oil outlet pipeline.
In the process of implementing the invention, the inventor finds that the related art has at least the following problems: firstly, the water blending amount lacks theoretical basis, and the water blending amount is mainly determined by a water testing method at present, and the water blending water nozzle is replaced step by depending on production experience to determine the water blending amount. And secondly, in a double-pipe water mixing flow, each oil well is matched with one water mixing pipeline and one oil outlet pipeline, so that the problems of complex process, large engineering quantity, high investment and high energy consumption exist.
Disclosure of Invention
The embodiment of the invention provides a crude oil gathering and transportation method which can optimize the water blending amount and simplify the water blending process. The technical scheme of the embodiment of the application is as follows:
the embodiment of the application provides a crude oil gathering and transportation method, which is characterized by comprising the following steps:
determining the sorting of the gathering and transportation difficulty degree of each oil well according to the production data of each oil well in the oil field block;
sequentially connecting all oil wells in the oil field block in series from high gathering and transportation difficulty degree to low gathering and transportation difficulty degree according to the sorting of the gathering and transportation difficulty degree through an oil outlet pipeline;
performing rheological property test on the crude oil, and determining a gathering and transportation phase-transfer point of the crude oil, wherein the gathering and transportation phase-transfer point is the water content when the viscosity of the crude oil reaches the highest point;
obtaining the water mixing rate of the oil field block according to the oil production rate of the oil field block, the liquid production rate of the oil field block and the gathering, transportation and phase transition point of the crude oil;
and connecting a water mixing pipeline with the oil well with the highest gathering and transportation difficulty degree, and mixing water into the oil well with the highest gathering and transportation difficulty degree according to the water mixing rate so as to enable all the oil wells to carry out crude oil gathering and transportation through the oil outlet pipeline.
Optionally, the determining the ranking of the gathering difficulty level of each oil well comprises:
connecting pipelines with the same length and the same specification between all the oil wells and the united station;
fixing the station entering pressure of the pipeline into the combined station;
calculating the wellhead pressure of each oil well according to the inbound pressure and a hydraulic calculation formula by using process software;
the numerical value of the wellhead pressure is larger, the gathering difficulty degree is higher, and the ranking is higher.
Optionally, the determining the gathering difficulty level of each oil well comprises:
connecting all the oil wells with a united station by using pipelines with the same length and the same specification;
fixing the arrival temperature of the pipeline entering the combined station;
calculating the wellhead temperature of each oil well according to the inbound temperature and a thermodynamic calculation formula by using process software;
the smaller the value of the wellhead temperature is, the higher the gathering difficulty degree is, and the higher the ranking is.
Optionally, the determining the gathering difficulty level of each oil well comprises:
measuring the viscosity of the produced crude oil of each of the wells;
a higher value for the crude oil viscosity indicates a higher degree of difficulty in the gathering, the higher the ranking.
Optionally, said measuring the viscosity of the produced crude oil of each said oil well comprises:
collecting an oil sample of each oil well into a standard pipe of a falling ball viscometer, and using a super constant temperature water bath to keep the temperature of the oil sample in the standard pipe at the formation temperature;
rotating the standard pipe to enable the top of the falling ball viscometer to face downwards, and enabling the steel ball in the standard pipe to be attracted to the magnet on the top of the standard pipe;
rotating the standard pipe to enable the top of the standard pipe to face upwards, so that the standard pipe is inclined and fixed;
recording the time for the steel ball to fall from the top of the standard pipe to the bottom of the standard pipe;
the viscosity of the crude oil is obtained according to a first formula as follows:
μ0＝k(ρ1-ρ2)t
wherein,
μ0viscosity of the crude oil, mPa · s;
k-falling ball viscometer constant;
t is the time, s, for the steel ball to fall from the top of the standard tube of the falling ball viscometer to the bottom of the standard tube of the falling ball viscometer;
ρ1density of steel ball, g/cm3；
ρ2Oil sample Density, g/cm3。
Optionally, said recording the time said steel ball falls from the top to the bottom of said standard pipe comprises:
and opening a switch of the magnet to enable the steel ball to fall, starting timing, automatically stopping timing when the steel ball falls to the bottom of the standard pipe, and recording the falling time of the steel ball.
Repeating the test at least three times, and respectively recording the falling time of the steel ball each time;
the angle of inclination of the standard tube was changed at least three times and the test was repeated.
Optionally, the determining the gathering transphase point of the crude oil comprises:
measuring the relation between the viscosity and the water content of the crude oil;
and determining the water content of the crude oil when the viscosity of the crude oil reaches the highest point, wherein the water content is the gathering and transportation phase transition point.
Optionally, said deriving a water loading rate for said field block from an oil production rate for said field block, a fluid production rate for said field block, and said terminal oil transfer point, comprises:
calculating the water mixing rate of all oil wells in the oil field block according to the following second formula:
wherein,
a-production rates of all wells within the field block;
b-the production rate of all wells in the field block;
c-the gathering and transportation phase inversion point of the crude oil produced by the oil well in the oil field block;
d-water doping rates for all wells in the field block.
Optionally, said deriving a water loading rate for said field block from an oil production rate for said field block, a fluid production rate for said field block, and said terminal oil transfer point, comprises:
and calculating the single-well water mixing rate of each oil well in the oil field block according to the following second formula:
adding the water mixing rates of the single wells of each oil well in the oil field block to obtain the water mixing rates of all the oil wells in the oil field block;
wherein,
a-individual well production rate for each well within the field block;
b-individual well production rate for each well within the field block;
c-gathering and transferring phase points of crude oil produced by each well within the field block;
d-Single well Water-doping Rate for each well within the oilfield block.
The method for gathering and transporting the crude oil provided by the embodiment of the application has the beneficial effects that at least:
the crude oil gathering and transporting method provided by the embodiment of the application can determine the gathering and transporting difficulty degree of each oil well according to the production data of each oil well in the oil field block, sequence is sequentially carried out according to the gathering and transporting difficulty degree from high to low, the well-sequenced oil wells are sequentially connected in series through the oil outlet pipeline, only one oil outlet pipeline is needed to be connected between every two oil wells, the length of the water mixing pipeline can be reduced, and materials are saved. And the water blending rate of the blended water required by all the oil wells is calculated through the liquid production rate and the oil production rate of all the oil wells in the oil field block and the technical phase transition point of the crude oil, so that the blended water is only required to be injected into one oil well, namely, the blended water is only injected into the oil well which is most difficult to gather and transport, the blended water and the produced liquid of the oil well flow through the oil outlet pipeline together, the water content of the crude oil of other subsequent oil wells is improved, all the oil wells are connected in series through the oil outlet pipeline, and the normal gathering and transport of the crude oil of all the oil wells can be ensured while the water blending amount is determined, the water blending flow is simplified. The gathering, transportation and phase inversion point of the crude oil, namely the water content of the crude oil when the viscosity of the crude oil reaches the maximum, can be determined by performing a rheological test on the crude oil. After the gathering and transportation phase transfer point of the oil well is determined, when the water is actually mixed in the oil well, the water content of the crude oil of all the oil wells is ensured to be higher than the gathering and transportation phase transfer point, and the optimization of the water mixing amount is realized. The method completely injects the water mixing rate required to be injected by all oil wells into the oil well which is the most difficult to collect and transport, and all the oil wells are connected in series through the oil outlet pipeline, namely, all the oil wells are mixed with water, the operation is simple, the material is saved, and the flow of collecting and transporting the crude oil of all the oil wells is simplified.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings used in the description of the embodiments will be briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained based on these drawings without creative efforts.
FIG. 1 is a flow chart of a crude oil gathering and transportation method provided by an embodiment of the present application;
FIG. 2 is a flow chart of a first method for implementing the method for determining the most difficult well to gather according to the embodiment of the present application;
FIG. 3 is a flow chart of a second method of implementing the method for determining the most difficult wells for gathering and transporting according to the embodiment of the present application;
FIG. 4 is a flow chart of a third method for implementing the method for determining the most difficult well for gathering provided by the embodiment of the present application;
FIG. 5 is a flow chart for measuring the viscosity of crude oil provided by an embodiment of the present application;
FIG. 6 is a flow chart for recording the time when a steel ball falls from the top of a standard pipe to the bottom of the standard pipe according to the embodiment of the present application;
FIG. 7 is a flow chart for obtaining a transition point of an oil well set according to an embodiment of the present disclosure;
fig. 8 is a schematic structural diagram of a falling ball viscometer provided in an embodiment of the present application.
The reference numerals in the figures denote:
1-a base;
2-a scaffold;
3-test tube clamp;
4-standard pipe;
5-steel ball;
6-magnet.
Detailed Description
Reference will now be made in detail to exemplary embodiments, examples of which are illustrated in the accompanying drawings. Where the following description refers to reference numerals, the same reference numerals in different embodiments refer to the same or similar elements unless otherwise indicated.
The embodiments described in the following exemplary embodiments do not represent all embodiments consistent with the present invention. Rather, they are merely examples of structures consistent with certain aspects of the invention, as detailed in the appended claims.
The embodiment of the application provides a crude oil gathering and transportation method, and referring to fig. 1, the method comprises the following steps:
step S1, determining the sorting of the gathering and transportation difficulty degree of each oil well according to the production data of each oil well in the oil field block.
For example, in the present embodiment, the wells are piped to produce crude oil to a cogeneration or relay station, production data is collected from all wells in the field, and the ranking of the technical difficulty level for each well is determined from the production data for each well individually. Wherein, this production data can include the individual well oil production, individual well moisture content, crude oil freezing point, crude oil density, well head temperature, the temperature and the pressure of joint station of every oil well.
For example, referring to fig. 2, in a first implementation manner of the embodiment of the present application, the step S1 may include:
and S101, connecting pipelines with the same length and the same specification between all oil wells and the united station.
For example, in a first implementation of the embodiments of the present application, in order to allow accuracy in determining the gathering difficulty of all wells, each well may be connected to a combination station using the same length and the same size of tubing, thus ensuring that the external conditions affecting the gathering difficulty of the wells are consistent.
And S102, fixing the arrival pressure of the pipeline entering the combined station.
For example, in a first implementation manner of the embodiment of the present application, the pressure at the end of the pipeline connected to all oil wells, that is, the station entering pressure when the pipeline connected to all oil wells enters the united station, is fixed to a uniform value, so as to ensure that the pressure values at all crude oil gathering and transportation terminals are uniform.
And step S103, calculating the wellhead pressure of each oil well according to the inbound pressure and a hydraulic calculation formula by using process software.
For example, in a first implementation manner of the embodiment of the present application, the pressure value of the wellhead during crude oil gathering of each oil well can be calculated according to the production data of each oil well, the pressure of the union station at the fixed pipeline terminal and a corresponding hydraulic calculation formula. The oil outlet pipeline of the oil well is mostly gas-liquid mixed phase flow, and the design parameters are more, so that hydraulic calculation formulas related to the pressure of the wellhead of the oil well, the pipeline station entering pressure and the property parameters of oil produced by the oil well can be set in advance through process software, and the pressure of each wellhead of the oil well is calculated according to the software.
And step S104, the oil wells with the higher numerical values of the wellhead pressures indicate that the gathering and transportation difficulty degree is higher, and the ranking is higher.
For example, in a first implementation manner of the embodiment of the present application, determining the difficulty level of gathering and transporting the oil well refers to the pressure at the wellhead of the oil well during the gathering and transporting of the crude oil, and the greater the wellhead pressure is, the more difficult the gathering and transporting of the crude oil is. Thus, when the pressure at which the pipes of all wells enter the united station is set to a uniform value, the property parameters of the oil produced by each well are different, and the pressure at the wellhead of the well is also different.
For example, in practical applications, the wellhead pressure of each oil well is different, and the pressure when the oil well is finally transmitted to the combination station is also different, if the wellhead pressure of each oil well is detected only, since the pressure of the oil well in the oil production process may change in real time, the wellhead pressure is also affected when the oil well at different time instants produces oil, and the detected wellhead pressure may cause the detected wellhead pressure to be inaccurate due to time factors.
Therefore, in the first implementation manner of the embodiment of the application, the pressure when the pipeline is transmitted to the joint station can be fixed at a value, the pipeline connected between each oil well and the joint station is also set to be the same in length and specification, and the wellhead pressure of each oil well is calculated according to the property parameters of the produced oil of different oil wells, so that the accuracy of the calculated wellhead pressure of each oil well can be ensured to a certain extent, and the gathering and transportation difficulty degree of each oil well is determined according to the wellhead back pressure of each oil well calculated by software.
And obtaining the wellhead pressure of each oil well through software, recording the wellhead pressure of each oil well, and sequencing all the oil wells from high to low according to the wellhead pressure according to the gathering and transportation difficulty degree.
Of course, the embodiments of the present application are not limited thereto, and in other implementations of the embodiments of the present application, the difficulty level of gathering and transporting all oil wells may also be determined by temperature or viscosity of crude oil or other parameters.
Alternatively, referring to fig. 3, in a second implementation manner of the embodiment of the present application, the step S1 may include:
and step S111, connecting all oil wells with the united station by using pipelines with the same length and the same specification.
For example, in a second implementation manner of the embodiment of the present application, the temperature of the wellhead can be used as a criterion for judging the difficulty level of oil well gathering. Firstly, pipelines with the same length and the same specification can be used for connecting each oil well with the combined station, the accuracy of determining the gathering and transportation difficulty degree of all the oil wells is ensured, and the consistency of external conditions influencing the gathering and transportation difficulty degree of the oil wells can be ensured.
And step S112, fixing the arrival temperature of the pipeline entering the united station.
For example, in the second implementation manner of the embodiment of the present application, the temperature of the terminal of the pipeline connected to all oil wells, that is, the entering temperature when the pipeline connected to all oil wells enters the united station, is fixed to a uniform value, so as to ensure that the temperature values of all crude oil gathering and transportation terminals are uniform. In this implementation manner of the embodiment of the present application, the gathering and transportation difficulty level of each oil well can be judged according to the temperature.
And step S113, calculating the wellhead temperature of each oil well according to the inbound temperature and a thermodynamic calculation formula by using process software.
For example, in a second implementation manner of the embodiment of the present application, a temperature value of a wellhead during the production process of each oil well can be calculated according to the production data of each oil well, the temperature of the union station at the fixed pipeline end point and a corresponding thermodynamic calculation formula. The oil outlet pipeline of the oil well is mostly gas-liquid mixed phase flow, and the design parameters are more, so that a thermodynamic calculation formula related to the temperature of the wellhead of the oil well, the pipeline station entering temperature and the property parameters of oil produced by the oil well can be set in advance through process software, and the temperature of each wellhead of the oil well is calculated according to the software.
For example, the temperature of the crude oil before transmission can be obtained according to the temperature of the crude oil when the crude oil enters the united station, the property parameters of the oil produced by the corresponding oil well and a thermodynamic calculation formula, and the oil produced by the oil well just before transmission can be transmitted only by heating the oil to enable the temperature to rise to a certain specific value, that is, the temperature of the crude oil when the crude oil starts to be transmitted is greater than the temperature of a well mouth, so that the temperature of the well mouth of the corresponding oil well can be obtained through calculation, the smaller the temperature of the well mouth is, the higher the gathering and transmission difficulty degree of the corresponding oil well is, and the more the ranking is.
Alternatively, if the temperatures of all the wells at the time of starting the transportation of the crude oil are the same, the gathering difficulty level of the corresponding well may be determined based on the temperature difference between the temperature at the time of starting the transportation of the crude oil and the wellhead temperature of the well at the time of just producing the oil from the well, and the wells with larger temperature differences may indicate that the gathering difficulty level is higher and the ranking is higher.
In step S114, the smaller the value of the wellhead temperature, the higher the gathering difficulty degree is, and the higher the ranking is.
For example, in a second implementation of the embodiments of the present application, temperature affects the viscosity of oil, and as the wellhead temperature is lower, that is, the temperature of oil just produced by the oil well is lower, the viscosity of produced oil is higher, the oil is less fluid, the pressure of transported oil is higher, and therefore the gathering difficulty is higher and the ranking is higher.
And obtaining the wellhead temperature of each oil well through software, recording the wellhead temperature of each oil well, and sequencing all the oil wells from high to low according to the gathering and transportation difficulty degree according to the wellhead temperature.
In the second implementation manner of the embodiment of the present application, the wellhead temperature refers to the temperature of oil just produced by an oil well, and since the temperature of oil just produced is low and cannot be directly transferred, the temperature of oil just produced is raised, and then the oil is transferred after reaching a predetermined temperature, and the temperature of oil reaching the predetermined temperature after being raised is referred to as a transfer start temperature.
Alternatively, referring to fig. 4, in a third implementation manner of the embodiment of the present application, the step S1 may include:
step S121, the viscosity of the produced crude oil of each well is measured.
For example, referring to fig. 5, in an implementation manner of the embodiment of the present application, the step S121 may include:
and S1211, collecting the oil sample of each oil well into a standard pipe of a falling ball viscometer, and keeping the temperature of the oil sample in the standard pipe at the bottom layer temperature by using a super constant temperature water bath.
For example, in one implementation of the embodiment of the present application, referring to fig. 8, the falling ball viscometer may include a base 1, a stand 2, a test tube clamp 3, and a standard tube 4, a magnet 6 may be disposed on the top of the standard tube 4, and a steel ball 5 may be disposed inside the standard tube 4. The support 2 is vertically fixed on the base 1, one end of the test tube clamp 3 can be arranged on the support 2, the other end of the test tube clamp 3 can be used for clamping the standard tube 4, and one end, clamped by the standard tube 4, of the test tube clamp 3 can drive the standard tube 4 to rotate. Of course, the present application is not limited thereto, and in other implementations of the embodiments of the present application, the viscosity of the crude oil may be measured by other viscometers with reasonable structures.
And respectively collecting an oil sample of each oil well into the standard pipe 4, and keeping the temperature of the oil sample in the standard pipe 4 at the formation temperature by using super constant-temperature water bath, namely keeping the oil sample in a state just after the oil sample is produced.
In step S1212, the standard tube 4 of the falling ball viscometer is rotated to bring the top of the standard tube 4 downward, and the steel ball 5 in the standard tube 4 is attracted to the magnet 6 on the top of the standard tube 4.
In one implementation of the embodiment of the present application, the standard pipe 4 can be rotated so that the top of the standard pipe 4 faces downward, so that the steel ball 5 can be attracted to the magnet 6 by gravity and the attraction force of the magnet.
In step S1213, the standard tube 4 of the falling ball viscometer is rotated with the top of the standard tube 4 facing upward, so that the standard tube 4 is tilted and fixed.
For example, in one implementation of the embodiment of the present application, after the steel ball 5 is attracted to the magnet 6, the standard pipe 4 is rotated again so that the top is turned upward again, and the standard pipe 4 is tilted at an angle to fix the standard pipe 4.
In step S1214, the time for the steel ball 5 to fall from the top of the standard tube 4 to the bottom of the standard tube 4 of the falling ball viscometer is recorded.
For example, referring to fig. 6, in an implementation manner of the embodiment of the present application, the step S1314 may include:
step S12141 is to turn on the switch of the magnet 6 to start the dropping of the steel ball 5 and to start timing, and to automatically stop timing when the steel ball 5 drops to the bottom of the standard tube 4, and to record the dropping time of the steel ball 5.
For example, in one implementation manner of the embodiment of the present application, after the standard pipe 4 is fixed, the switch of the magnet 6 on the top of the standard pipe 4 may be opened, so that the steel ball 5 falls under the action of gravity, and the steel ball 5 is not attracted by the magnet 6 during the falling process, so that only the oil sample in the standard pipe 4 and the gravity on the steel ball 5 affect the falling of the steel ball 5.
An automatic timing device can be arranged on the standard pipe 4 of the viscometer, when the switch of the magnet 6 is turned on, the device automatically starts timing, and when the steel ball 5 falls to the bottom, the timing is automatically stopped, so that the falling time of the steel ball 5 in the oil sample can be accurately recorded.
In step S12142, the test is repeated at least three times, and the time of each drop of the steel ball 5 is recorded.
For example, the steps S1211 to S12141 are repeated at least three times without changing the inclination angle of the standard tube 4, the time of each fall of the steel ball 5 is recorded, and the results of the plurality of tests at the same inclination angle are obtained, and the average value is taken as the time of the fall of the steel ball 5 at the inclination angle.
Of course, the number of tests is not limited to this, and when the test result difference is larger under the same inclination angle, more tests can be performed to ensure the accuracy of the test result.
In step S12143, the angle of inclination of the standard pipe 4 is changed at least three times and the test is repeated.
For example, in one implementation of the embodiment of the present application, after three times of tests are performed on the same inclination angle, the inclination angle of the standard tube 4 may be changed, and after each time the inclination angle of the standard tube 4 is changed, the steps S1211 to S12142 are repeated to obtain the time for the steel ball 5 to fall after the inclination angle of the standard tube 4 is changed.
The inclination angle of the standard tube 4 may then be changed again, and the operation steps S121 to S12142 may be repeated again to obtain the corresponding time for the steel ball 5 to fall again. And recording the falling time of the steel ball 5 under different inclination angles for each oil well.
In step S1215, the viscosity of the crude oil is calculated according to the following first formula:
μ0＝k(ρ1-ρ2)t
wherein,
μ0viscosity of the crude oil, mPa · s;
k-falling ball viscometer constant;
t is the time, s, for the steel ball to fall from the top of the standard tube of the falling ball viscometer to the bottom of the standard tube of the falling ball viscometer;
ρ1density of steel ball, g/cm3；
ρ2Oil sample Density, g/cm3。
In an implementation manner of the embodiment of the present application, the constant of the falling ball viscometer is related to the inclination angle of the standard pipe 4, the density and the size of the steel ball 5, that is, the viscosity of the oil sample of each oil well at different inclination angles is obtained according to the falling time of the steel ball 5 at different angles, the constant of the standard pipe 4 at different angles, the density of the steel ball 5 and the density of the oil sample, and then the viscosity of the produced oil corresponding to the oil well is obtained.
Of course, the method for measuring the viscosity of the crude oil is not limited thereto, and in other implementations of the embodiments of the present application, other reasonable methods may be used to measure the viscosity of the crude oil.
In step S122, the higher the value of the crude oil viscosity, the higher the difficulty of gathering and transportation, and the higher the ranking.
For example, in the third implementation manner of the embodiment of the present application, the viscosity of the produced crude oil of each oil well is measured, and the gathering difficulty level of the oil well is judged according to the viscosity of the crude oil, wherein the higher the viscosity of the crude oil produced by the oil well is, the poorer the fluidity of the oil is, and the higher the gathering difficulty level of the oil well is, the higher the ranking is.
For example, in a third implementation of the embodiments of the present application, the viscosities of the crude oils produced by all the wells in the reservoir block may be detected experimentally, the viscosity of the crude oil produced by each well may be recorded, and all the wells may be ranked according to their viscosities from large to small in the difficulty level of gathering and transportation.
In addition, the method for determining the gathering and transportation difficulty level of each oil well in the embodiment of the present application is not limited to this, and in other implementation manners of the embodiment of the present application, the gathering and transportation difficulty level of each oil well may be determined according to other reasonable parameters.
And step S2, sequentially connecting all oil wells in the oil field block in series from high gathering and transportation difficulty level to low gathering and transportation difficulty level according to the sorting of the gathering and transportation difficulty level through the oil outlet pipeline.
For example, in an implementation manner of the embodiment of the present application, after the gathering and transportation difficulty levels of each oil well are recorded and sequenced, all the oil wells in an oil field block may be sequentially connected in series from high to low according to the gathering and transportation difficulty levels through the oil outlet pipeline, that is, an oil outlet pipeline may be connected between every two oil wells with a close gathering and transportation difficulty level, so that all the oil wells may be connected in series, and thus, only the oil well with the highest gathering and transportation difficulty level needs to be watered, the oil outlet pipeline of the oil well with a higher gathering and transportation difficulty level is the watering pipeline of the next oil well, all the oil wells are communicated, so that the watered water may flow through all the oil wells, and the watered water is watered to all the oil wells, thereby saving pipeline materials and optimizing the watering process.
And step S3, performing rheological test on the crude oil, and determining the gathering, transportation and phase inversion point of the crude oil.
For example, in one implementation of the embodiments herein, a rheological test may be performed on the crude oil to determine a property parameter of the crude oil. For example, a rheology test for crude oil may include determining the viscosity of the crude oil as a function of temperature and the viscosity of the crude oil as a function of water cut.
In the process of crude oil transmission, shear stress can be generated on crude oil due to mutual friction between the crude oil and a transport pipe wall, the viscosity of the crude oil can be influenced by different shear stress or shear rate, and the ratio of the shear stress to the shear rate received by the crude oil is the viscosity of the crude oil. The viscosity of the crude oil is more affected by the shear rate when the temperature of the crude oil is below the point of failure of the crude oil, the greater the shear rate the lower the viscosity of the crude oil, but the shear rate has less effect on the viscosity of the crude oil when the temperature is above the point of failure. Moreover, at a relatively high temperature, the lower the viscosity of the crude oil, the lower the anomaly point of the crude oil is, i.e., the transition of the crude oil from the non-Newtonian fluid state to the Newtonian fluid state. Therefore, the temperature should be raised above the abnormal point during the transportation of the crude oil, so as to ensure the fluidity of the crude oil and reduce the influence of the shear stress on the viscosity of the crude oil during the transportation of the crude oil.
In the present embodiment, the gathering and transportation phase inversion point refers to the water content of the crude oil at which the viscosity of the crude oil reaches the maximum. For example, referring to fig. 7, this step may include:
step S31, the relation between the viscosity and the water content of the crude oil is measured.
Collecting crude oil produced by an oil well, adding water into the crude oil, monitoring the water content of the crude oil and the viscosity of the crude oil in real time, and determining the relation between the viscosity of the crude oil and the water content.
And step S32, determining the water content of the crude oil when the viscosity of the crude oil reaches the highest point, wherein the water content at the moment is the gathering and transportation phase inversion point.
From the relationship between the viscosity and the water content of the crude oil, it is known that when the water content of the crude oil is lower than a certain value, the viscosity of the crude oil rises with the rise of the water content, and when the water content of the crude oil is higher than the certain value, the viscosity of the crude oil drops sharply with the rise of the water content, and therefore, the value is the gathering, transportation and phase transition point of the crude oil.
The gathering and transferring phase point may be a gathering and transferring phase point of a mixed oil sample of crude oil produced by all oil wells in the same oil field block, or may be a technical transferring phase point of crude oil produced by any oil well in the oil field block, or may also be a gathering and transferring phase point of crude oil produced by each oil well in the oil field block.
In an implementation manner of the embodiment of the application, crude oil produced by an oil well is collected, a gathering and transportation phase inversion point is determined by developing a rheological test of the crude oil, and because factors such as geology, environment and the like in the same oil field block are almost the same, the crude oil of any oil well in the oil field block can be collected only when the gathering and transportation phase inversion point is determined.
Of course, the present application is not limited thereto, and in another implementation manner of the embodiment of the present application, the crude oil produced by each well may be collected, and the gathering and transferring phase point of the produced crude oil of each well may be determined separately. Alternatively, a mixed oil sample of the crude oil produced by all the oil wells in the oil field block can be collected, and the gathering and transferring phase point of the mixed oil sample can be determined by performing a crude oil rheological test on the mixed oil sample.
And step S4, obtaining the water mixing rate required by the oil wells in the oil field block according to the oil production rate of the oil wells in the oil field block, the liquid production rate of the oil field block and the crude oil gathering, transportation and phase transition point.
For example, in one implementation of the embodiments of the present application, the oil production rate and the fluid production rate of all the oil wells in the field block can be obtained according to the oil production and the fluid production per hour of all the oil wells in the field block, and then the water blending rate required by all the oil wells in the field block can be obtained according to the following second formula by combining the gathering and transferring phase point of the crude oil produced by the oil wells in the field block:
wherein, in the realization mode of the embodiment of the application,
a-the production rate of all wells in the field block;
b-production rates of all wells in the field block;
c-the gathering, transportation and phase inversion point of the crude oil produced by the oil well in the oil field block;
d-water doping rates for all wells in the field block.
Specifically, in order to ensure that the water content of all oil wells is higher than the gathering and transportation phase inversion point as much as possible, the comprehensive water content after the water blending is higher than the gathering and transportation phase inversion point by 10%, of course, the present application is not limited thereto, and in other implementation manners of the embodiments of the present application, the gathering and transportation phase inversion point may be increased by other values.
The gathering and transferring phase point can be a gathering and transferring phase point of a mixed oil sample of crude oil produced by all oil wells in the oil field block, and can also be a gathering and transferring phase point of crude oil produced by any oil well in the oil field block.
And then dividing the oil production rate of the oil field block by the comprehensive water content after water blending to obtain the theoretical liquid production rate after water blending, and subtracting the liquid production rate of the oil field block before water blending to obtain the required water blending rate.
For example, in another implementation of the embodiments of the present application, the gathering transition point of the crude oil produced by each well may be determined separately, and then the single-well fluid production rate of each well and the single-well oil production rate of each well are collected separately, and the water-blending rate required for each well is obtained according to the second formula:
wherein, in the realization mode of the embodiment of the application,
a-individual well production rate for each well within the field block;
b-individual well production rate for each well in the field block;
c-gathering and transportation phase inversion point of crude oil produced by each well in the oilfield block;
d-Single well Water-Per well Rate in the oilfield block.
The water blending rates required by each well are then summed to obtain the water blending rates required by all wells in the field block.
And step S5, connecting the water mixing pipeline with the oil well with the highest gathering and transportation difficulty degree, and mixing water into the oil well with the highest gathering and transportation difficulty degree according to the obtained water mixing speed, so that all the oil wells can gather and transport crude oil through the oil outlet pipeline.
For example, in the embodiment of the present application, after obtaining the water blending rate required by all the oil wells in the field block, the water blending pipeline from the united station or the transfer station can be connected to the oil well with the highest difficulty in transportation, and then the water is blended into the oil well, and the blended water is mixed with the produced crude oil to increase the water content of the crude oil produced by the oil well, so as to improve the fluidity of the crude oil produced by the oil well.
Then connect the next oil well of gathering and transporting the second highest degree of difficulty by oil outlet pipe, improve the moisture content of the crude oil of this oil well output and then improve the mobility of oil. And then the next oil well is connected through the oil outlet pipeline of the oil well with the second highest gathering and transportation difficulty degree, so that the circulation is realized, the tax rate of the crude oil produced by all the oil wells is improved, and the flowability of the crude oil is ensured. Therefore, only one water-mixing pipeline can be connected, so that the construction of the water-mixing pipeline is greatly reduced, and the engineering investment is reduced.
The foregoing is a more detailed description of the present invention in connection with specific preferred embodiments thereof, and it is not intended that the specific embodiments of the present invention be limited to these descriptions. For those skilled in the art to which the invention pertains, other embodiments that do not depart from the gist of the invention are intended to be within the scope of the invention.
Claims (9)
1. A method of gathering crude oil, comprising:
determining the sorting of the gathering and transportation difficulty degree of each oil well according to the production data of each oil well in the oil field block;
sequentially connecting all oil wells in the oil field block in series from high gathering and transportation difficulty degree to low gathering and transportation difficulty degree according to the sorting of the gathering and transportation difficulty degree through an oil outlet pipeline;
performing rheological property test on the crude oil, and determining a gathering and transportation phase-transfer point of the crude oil, wherein the gathering and transportation phase-transfer point is the water content when the viscosity of the crude oil reaches the highest point;
obtaining the water mixing rate of the oil field block according to the oil production rate of the oil field block, the liquid production rate of the oil field block and the gathering, transportation and phase transition point of the crude oil;
and connecting a water mixing pipeline with the oil well with the highest gathering and transportation difficulty degree, and mixing water into the oil well with the highest gathering and transportation difficulty degree according to the water mixing rate so as to enable all the oil wells to carry out crude oil gathering and transportation through the oil outlet pipeline.
2. The method of claim 1, wherein said determining the ranking of the gathering difficulty level for each well comprises:
connecting pipelines with the same length and the same specification between all the oil wells and the united station;
fixing the station entering pressure of the pipeline into the combined station;
calculating the wellhead pressure of each oil well according to the inbound pressure and a hydraulic calculation formula by using process software;
the numerical value of the wellhead pressure is larger, the gathering difficulty degree is higher, and the ranking is higher.
3. The method of claim 1, wherein said determining the level of difficulty of gathering each of said oil wells comprises:
connecting all the oil wells with a united station by using pipelines with the same length and the same specification;
fixing the arrival temperature of the pipeline entering the combined station;
calculating the wellhead temperature of each oil well according to the inbound temperature and a thermodynamic calculation formula by using process software;
the smaller the value of the wellhead temperature is, the higher the gathering difficulty degree is, and the higher the ranking is.
4. The method of claim 1, wherein said determining the level of difficulty of gathering each of said oil wells comprises:
measuring the viscosity of the produced crude oil of each of the wells;
a higher value for the crude oil viscosity indicates a higher degree of difficulty in the gathering, the higher the ranking.
5. The method of claim 4, wherein said measuring the viscosity of the produced crude oil of each oil well comprises:
collecting an oil sample of each oil well into a standard pipe (4) of a falling ball viscometer, and maintaining the temperature of the oil sample in the standard pipe (4) at the formation temperature by using a super constant temperature water bath;
rotating the standard pipe (4) to enable the top of the falling ball viscometer to face downwards, and enabling a steel ball (5) in the standard pipe (4) to be attracted to a magnet (6) on the top of the standard pipe (4);
rotating the standard pipe (4) to enable the top of the standard pipe (4) to face upwards, so that the standard pipe (4) is inclined and fixed;
recording the time for the steel ball (5) to fall from the top of the standard pipe (4) to the bottom of the standard pipe (4);
the viscosity of the crude oil is obtained according to a first formula as follows:
μ0＝k(ρ1-ρ2)t
wherein,
μ0viscosity of the crude oil, mPa · s;
k-falling ball viscometer constant;
t is the time, s, for the steel ball to fall from the top of the standard tube of the falling ball viscometer to the bottom of the standard tube of the falling ball viscometer;
ρ1density of steel ball, g/cm3；
ρ2Oil sample Density, g/cm3。
6. Crude oil gathering and transportation method according to claim 5, characterized in that said recording the time of the steel ball (5) falling from the top to the bottom of the standard pipe (4) comprises:
opening a switch of the magnet (6) to enable the steel ball (5) to fall, starting timing, automatically stopping timing when the steel ball (5) falls to the bottom of the standard pipe (4), and recording the falling time of the steel ball (5);
repeating the test at least three times, and respectively recording the time of each falling of the steel ball (5);
the angle of inclination of the standard tube (4) is changed at least three times, and the test is repeated.
7. The method of claim 1, wherein determining the gathering transition point of the crude oil comprises:
measuring the relation between the viscosity and the water content of the crude oil;
and determining the water content of the crude oil when the viscosity of the crude oil reaches the highest point, wherein the water content is the gathering and transportation phase transition point.
8. The method of claim 1, wherein the deriving the water loading rate of the field block from the oil production rate of the field block, the fluid production rate of the field block, and the trans-phase point of the crude oil comprises:
calculating the water mixing rate of all oil wells in the oil field block according to the following formula:
wherein,
a-production rates of all wells within the field block;
b-the production rate of all wells in the field block;
c-the gathering and transportation phase inversion point of the crude oil produced by the oil well in the oil field block;
d-water doping rates for all wells in the field block.
9. The method of claim 1, wherein the deriving the water loading rate of the field block from the oil production rate of the field block, the fluid production rate of the field block, and the trans-phase point of the crude oil comprises:
calculating the single-well water mixing rate of each oil well in the oil field block according to the following formula:
adding the water mixing rates of the single wells of each oil well in the oil field block to obtain the water mixing rates of all the oil wells in the oil field block;
wherein,
a-individual well production rate for each well within the field block;
b-individual well production rate for each well within the field block;
c-gathering and transferring phase points of crude oil produced by each well within the field block;
d-Single well Water-doping Rate for each well within the oilfield block.
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201381836Y (en) * | 2009-01-12 | 2010-01-13 | 西安长庆科技工程有限责任公司 | Oilfield multiwell short-distance cascading oil collecting device |
| CN102095079A (en) * | 2009-12-10 | 2011-06-15 | 戈宝富 | Water-blended gathering and transferring process technology |
| CN205859613U (en) * | 2016-06-30 | 2017-01-04 | 中国石油天然气股份有限公司 | Oil well water-mixing oil-collecting process system |
| CN106764429A (en) * | 2016-12-27 | 2017-05-31 | 鲍云波 | The continuous closed gathering system of individual well branch line ring-type ground crude oil and the continuous closed gathering method of crude oil |
| CN206376844U (en) * | 2017-01-20 | 2017-08-04 | 中国石油化工股份有限公司 | Oil well high and low pressure water mixing automatic transfer equipment |
-
2018
- 2018-12-20 CN CN201811562692.3A patent/CN111350943B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201381836Y (en) * | 2009-01-12 | 2010-01-13 | 西安长庆科技工程有限责任公司 | Oilfield multiwell short-distance cascading oil collecting device |
| CN102095079A (en) * | 2009-12-10 | 2011-06-15 | 戈宝富 | Water-blended gathering and transferring process technology |
| CN205859613U (en) * | 2016-06-30 | 2017-01-04 | 中国石油天然气股份有限公司 | Oil well water-mixing oil-collecting process system |
| CN106764429A (en) * | 2016-12-27 | 2017-05-31 | 鲍云波 | The continuous closed gathering system of individual well branch line ring-type ground crude oil and the continuous closed gathering method of crude oil |
| CN206376844U (en) * | 2017-01-20 | 2017-08-04 | 中国石油化工股份有限公司 | Oil well high and low pressure water mixing automatic transfer equipment |
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